Composition and method for coke retardant during pyrolytic hydrocarbon processing

ABSTRACT

The present invention is directed to a method of inhibiting the formation of coke during the elevated temperature cracking of hydrocarbons. The method generally comprises adding to the hydrocarbon an effective amount of an ammonium borate, particularly ammonium biborate and ammonium pentaborate. Preferably, the ammonium borates are in a glycollic solvent or water.

BACKGROUND OF THE INVENTION

The present invention is directed to a method and composition for use ininhibiting the formation and deposition of coke on surfaces during theelevated temperature processing of hydrocarbons. Coke deposition isgenerally experienced when hydrocarbon liquids and vapors contact thehot metal surfaces of the processing equipment. While perhaps notentirely technically understood, because of the complex makeup of thehydrocarbons, the hydrocarbons at elevated temperatures and in contactwith hot metallic surfaces undergo various changes through eitherchemical reactions and/or decomposition of various unstable componentsof the hydrocarbon. The undesired products in many instances includecoke, polymerized products, deposited impurities and the like. Whateverthe undesired product that may be formed, the result is the same, i.e.,reduced economies of the process. If these deposits are allowed toremain unchecked, heat transfer, throughput and overall productivity aredetrimentally effected. Moreover, downtime is likely to be encountereddue to the necessity of either replacing and/or cleaning of the affectedparts of the processing system.

While the formation and type of undesired products are dependent uponthe hydrocarbon being processed and the conditions of the processing, itmay generally be stated that such products can be produced attemperatures as low as 100° F.; but are much more prone to formation asthe temperature of the processing system and the metal surfaces thereofin contact with the hydrocarbon increase. At these temperatures, cokeformation is likely to be produced regardless of the type hydrocarbonbeing charged. The type coke formed, i.e., amorphous, filamentous orpyrolytic, may vary somewhat; however, the probability of the formationof such is quite high.

As indicated in U.S. Pat. Nos. 3,531,394 and 4,105,540 the teachings ofwhich are incorporated herein by reference, coke formation anddeposition are common problems in ethylene (olefin) plants which operateat temperatures where the metal surfaces in contact with the hydrocarbonare at 1600° F. and above. The problem is prevalent in the crackingfurnace coils as well as in the transfer line exchangers where pyrolytictype coke formation and deposition is commonly encountered. Ethyleneplants often referred to generally as "olefin plants", originallyproduced simple olefins such as ethylene, propylene, butanes andbutadiene from a feed of ethane, propane, butanes and mixtures thereof.Later developments in the area of technology however, has led to thecracking of heavier feedstocks because of their availability to producearomatics and pyrolysis gasoline as well as light olefins. Feedstocksnow include light naphtha, heavy naphtha and gas oil. According to thethermal cracking processes utilized in olefin plants, the feedstocks arecracked generally in the presence of steam in tubular pyrolysisfurnaces. The feedstock is preheated, diluted with steam and the mixtureheated in the pyrolysis furnace to about 1500° F. and above, most oftenin the range of 1500° to 1650° F. The effluent from the furnace israpidly quenched by direct means or in exchangers which are used togenerate high pressure steam at 400 to 800 psig for process use. Thisrapid quench reduces the loss of olefins by minimizing secondaryreactions. The cooled gas then passes to the prefractionator where it iscooled by circulating oil streams to remove the fuel oil fraction. Insome designs, the gas leaving the quench exchanger is further cooledwith oil before entering the prefractionator. In either case, the heatpicked up by the circulating oil streams is used to generate steam andto heat other process streams. The mixture of gas and steam leaving theprefractionator is further cooled in order to condense the steam andmost of the gasoline product in order to provide reflux for theprefractionator. Either a direct water quench or heat exchangers areused for this cooling duty.

After cooling, cracked gas at, or close to atmospheric pressure, iscompressed in a multistage compression system to much higher pressures.There are usually four or five stages of compression with interstagecooling and condensate separation between stages. Most plants havehydrocarbon condensate stripping facilities. Condensate from theinterstage knockout drums is fed to a stripper where the C₂ hydrocarbonsand lighter, are separated. The heavier hydrocarbons are fed to thedepropanizer.

While various treatments have been proposed to eliminate or reducefilamentous coke formation at elevated temperatures, none have attainedany great degree of success. In the book "Coke Formation on MetalSurfaces" by Albright and Baker, 1982, methods are described whichutilize silicon and aluminum as pretreatments. In accordance with theprocedure, the furnace tubes are pretreated with silicon and aluminumhours before introduction of the hydrocarbon feedstocks. With the use ofsilicon, furnace tubes are coated by the chemical vaporization of analkoxysilane. While U.S. Pat. Nos. 4,105,540 and 4,116,812 are generallydirected to fouling problems in general, the patents disclose the use ofcertain phosphate and phosphate and sulfur containing additives for usepurportedly to reduce coke formation in addition to general foulants athigh temperature processing conditions.

With respect to coke retardation, various efforts have been reported,namely:

1. French Pat. No. 2,202,930 (Chem. Abstracts Vol. 83, 30687K) isdirected to tubular furnace cracking of hydrocarbons where molten oxidesor salts of group III, IV or VIII metals (e.g., molten lead containing amixture of K₃ VO₄, SiO₂ and NiO) are added to a pretested charge of, forexample, naphtha/steam at 932° F. This treatment is stated as havingreduced deposit and coke formation in the cracking section of thefurnace.

2. Starshov et al, Izv Vyssh. Uchebn. Zaved., Neft GAZ, 1977 (Chem.Abst. Vol. 87: 154474r) describes the pyrolysis of hydrocarbons in thepresence of aqueous solutions of boric acid. Carbon deposits wereminimized by this process.

3. Nikonov et al., U.S.S.R. 834,107, 1981; (Chem. Abst. 95:135651v)describes the pyrolytic production of olefins with peroxides present ina reactor, the internal surfaces of which have been pretreated with anaqueous alcoholic solution of boric acid. Coke formation is notmentioned in this patent since the function of the boric acid is to coatthe inner surface of the reactor and thus decrease the scavenging ofperoxide radicals by the reactor surface.

4. Starshov et al., Neftekhimiya 1979 (Chem. Abst: 92:8645j) describesthe effect of certain elements including boron on coke formation duringthe pyrolysis of hydrocarbons to produce olefins.

5. U.S. Pat. No. 2,063,596 discusses in its prior art section theproblems associated with the processing of hydrocarbons in equipmentwhose metallic parts have been supplied with a metalloid. The generalimpression is that such has not been utilized successfully.

6. U.S. Pat. No. 1,847,095 in a somewhat ambiguous manner describes theuse of metalloid compounds such as boron hydride which are capable ofyielding "volatile hydrogen" during the processing of hydrocarbons. Thepatent is silent as regards the type of coke encountered and theproblems associated therewith and contains no disclosure or suggestionrelative to other boron compounds which may be utilized during theprocessing of hydrocarbons for protection against coke formation.

7. Baker, R.T.K., Gas Chem. Nucl. React. Large In dust. Plant, Proc.Conf., 1980. Chem. Ab. Vol. 94, 1981, 94:8141h, is directed to the roleof various additives e.g., B₂ O₃ in effecting the growth rate offilamentous coke produced from the decomposition of C₂ H₂ on Ni-Fe or MoCatalysts. B₂ O₃ is stated as being the only additive which failed toprovide any significant reduction in the growth of the filaments.

DESCRIPTION OF THE INVENTION

Generally the invention entails the use of certain boron compounds, andcompositions containing such, to inhibit the formation and deposition ofcoke on metallic surfaces in contact with a hydrocarbon (either inliquid or gaseous form) which surfaces reach temperatures of 1400° F.(or 1450° F.) and above (most often 1500°-2050° F.). These temperaturesare commonly encountered as earlier indicated in the olefin plants. Inthese systems the components of the furnace (pyrolytic) as well as theancillary parts are composed of ferrous metal. Iron, as well as ironalloys such as low and high carbon steel, and nickel-chromium-ironalloys are customarily used for the production of hydrocarbon processingequipment such as furnaces, transmission lines, reactors, heatexchangers, separation columns, fractionators, and the like.

The present inventor discovered that coking during the high temperaturescracking of hydrocarbons may be significantly reduced on the iron basedand nickel-based surfaces of processing equipment by adding to thehydrocarbon feed stock or charge before and/or during cracking, ammoniumborates and in particular ammonium pentaborates and biborates orcompositions containing such.

The ammonium borates are effective when formulated with glycollic-typesolvents, in particular ethylene glycol, propylene glycol and the likesince they produce marketable and easily fed solutions. Aqueoussolutions or simply water solutions of the ammonium borates are alsoeffective.

The ammonium borate compounds may be dissolved in the water or theglycol carriers in any proportions, to produce a product which willprovide the necessary amount of boron to any coke-formation proneenvironment to effectively eliminate or in the least minimize such.Coking is a significant problem and if left untreated will eventuallyshut the operation down. Accordingly it would be desirable to assurethat any product used is either high in boron content or if not high inboron content is fed to the charge at high dosage rates to assure theavailability of boron. Accordingly, product formulation lends itself togreat flexibility.

Generally the product can contain on a weight basis from about 1 to 50%ammonium borate, with the remainder being the carrier, for exampleethylene glycol. To assure maintenance of the solution during storageand exposure to different and perhaps drastic temperature conditions orto protect the solution during transportation, various stabilizingagents may also be added to the formulation as well as any preservativewhich might be desirable.

Typical formulations would be as follows:

    ______________________________________                                                          Percentage by Weight                                        Ingredient          Actual    Range                                           ______________________________________                                        Ammonium borate compound                                                                          10-15%     1-50                                           Solvent             90-85%    50-1                                            ______________________________________                                    

The treatment dosages again are dependent upon the severity of thecoking problem, location of such, and of course, the amount of boronbased compound in the formulated product. Perhaps the best method ofdescribing the treatment dosage would be based upon the actual amount of"boron" that should be added to the charge. Accordingly the amount offormulated product to be added to a charge should be such to provide 0.1ppm to 5,000 ppm, and preferably 0.5 ppm to 1000 ppm, of boron to saidhydrocarbon charge. When ammonium biborate or pentaborate is addedtogether with the carrier to the hydrocarbon feed stock in 0.1 to 5,000ppm (B), the borates are present in the combination in an amount of0.0001 to 2.5% by weight.

EXAMPLES

In order to establish the efficacy of the inventive concept varioustests were conducted utilizing a propane feedstock with dilution steamadded to enhance cracking. The apparatus and procedure used for thetesting were as follows:

Apparatus

The High Temperature Fouling Apparatus (HTFA) consists of fivesubsections which together simulate the pyrolysis of gaseoushydrocarbons to make light olefins and the coke formed on the heatedmetal surfaces during the pyrolysis reaction.

The feed preheat section is built of 316 stainless steel tubing andfittings and allows the mixing of nitrogen or oxygen containing gas withsteam during the bring up and shut down of the HTFA and the propane andsteam during the actual test. Steam is supplied at 40 psig by a steamgenerator and nitrogen, oxygen containing gas, or propane fromcompressed gas cylinders. The gases and steam are heated to about 400°F. at which point small amounts of water (blank test) or antifoulant isslowly injected into the stream by a syringe pump.

Following antifoulant injection, the gases flow through a coiled 316SStube inside an electrically heated furnace. The gases are heated to1100°-1200° F. at the furnace exit at a furnace temperature ofapproximately 1865° F.

Following the furnace tube, the gases travel through the coker rodassembly. This consists of a 316SS rod which is electrically heated to1500° F. while the gases flow around the heated rod inside a 316SSshell. The rod is electrically heated through a silicon controlledrectifier (SCR), then through two 4 to 1 stepdown transformers in seriesto achieve low voltage (3-4 volts), high amperage (≃200 amps) heating ofthe rod. A temperature controller is used to achieve power controlthrough the SCR to obtain a 1500° F. rod temperature.

Upon exiting the coker rod, the gases pass through a condenser coil andthen two knock-out flasks in ice baths to remove the water (steam) fromthe product gases. The remaining entrained water vapor in the gases isremoved by passing through drierite.

The specific gravity of the product gas is determined in a gasdensitometer and the gases analyzed using gas chromatography todetermine yields. The remaining gases are vented through a safety hoodexhaust.

Test Procedure

The furnace was turned on and the temperature thereof was stabilized at1200° F. with the coker rod reaching a temperature of 1500° F. whilefeeding nitrogen and steam. Oxygen feed containing gas and steam wasthen commenced and the furnace temperature permitted to increase toabout 1450° F. (requiring approximately 10 min.).

Nitrogen feed which was stopped during the oxygen containing gas feed,was then again initiated, and the rod temperature permitted to decreaseto 1200° F. Furnace temperatures were then slowly increased to 1800° F.over a period of 10 min. while the coke inhibitor or water (blank) asthe case may be was injected into the mixed gas/steam line prior to thefurnace at about 400° F. gas temperature.

The rod temperature was again increased to 1500° F., then nitrogen feedgradually switched to propane feed (about 2 min.). The temperature offurnace was then increased to about 1865° F. over approximately 30minute period. The product gases were analyzed by gas chromatography andthe temperatures, flowrates, pressures and product gas gravity recordedevery 35 minutes during the 160 min. test on propane/steam feed. Gasesexit the furnace tube at about 1150°-1250° F. and exit the coker shellat about 975°-1000° F. temperatures.

During a normal 160 minute run, approximately 3200-3300 grams of propaneare fed and 1500-2000 grams of steam (determined from the condensatecollected) for hydrocarbon to steam rates of about 1.6:1 to 2.2:1.

Following shutdown and cooling, the furnace tube and coker shell arecleaned and the coke collected and weighed. The coke is burned todetermine how much is non-coke (metal corrosion products). After aseries of blanks (water) and antifoulant tests are conducted, a steam tocoke relationship is determined for the blanks of A/x(condensate rate)and the predicted cokes compared to actual cokes of the treatments todetermine percent coke reduction.

Results

The data collected from the experiments using propane/steam feed andinjecting water during blanks (controls) or ammonium borate feeds areset forth below in Table 1.

                                      TABLE 1                                     __________________________________________________________________________    HTFA Data-Decoked Procedure-Propane Feed                                      Boron Containing Coke Retardants                                                                     Cond.      Non-                                                                              1  2                                                   Furnace                                                                            Run                                                                              Rate,                                                                              Coke                                                                             PPM                                                                              Coke                                                                              Pred                                                                             %                                    Additive                                                                              Solvent                                                                              Tube No.                                                                              Ml/Min                                                                             Gms.                                                                             B  Gms.                                                                              Coke                                                                             Prot                                 __________________________________________________________________________    Blank   H.sub.2 O                                                                            16    5 6.70 .94                                                                              0  .07 .91                                                                              -3                                   Blank   H.sub.2 O                                                                            15    2 8.00 .71                                                                              0  .09 .77                                                                               7                                   Blank   H.sub.2 O                                                                            16    6 6.00 1.15                                                                             0  .32 1.02                                                                             -13                                  Blank   H.sub.2 O                                                                            17    2 6.40 2.19                                                                             0  .05 .96                                                                              -129                                 Blank   H.sub.2 O                                                                            17    7 6.45 1.97                                                                             0  .06 .95                                                                              -107                                 Blank   H.sub.2 O                                                                            17   10 7.51 1.07                                                                             0  .11 .81                                                                              -31                                  Blank   H.sub.2 O                                                                            18    2 7.07 .32                                                                              0  .06 .87                                                                              63                                   Blank   H.sub.2 O                                                                            18   12 7.46 .66                                                                              0  .05 .82                                                                              20                                   Blank   H.sub.2 O                                                                            18   15 8.66 1.37                                                                             0  .13 .71                                                                              -94                                  Blank   H.sub.2 O                                                                            18   20 7.01 .55                                                                              0  .06 .87                                                                              37                                   Blank   H.sub.2 O                                                                            18   25 5.18 .43                                                                              0  .08 1.18                                                                             63                                   Blank   H.sub.2 O                                                                            19    2 6.55 .74                                                                              0  .20 .93                                                                              21                                   Blank   H.sub.2 O                                                                            19    8 6.43 .55                                                                              0  .12 .95                                                                              42                                   Blank   H.sub.2 O                                                                            19   13 8.64 1.14                                                                             0  .24 .71                                                                              -61                                  Blank   H.sub.2 O                                                                            19   19 9.22 .14                                                                              0  .07 .66                                                                              79                                   Blank   H.sub.2 O                                                                            19   20 7.88 .38                                                                              0  .11 .78                                                                              51                                   Blank   H.sub.2 O                                                                            19   27 4.13 2.74                                                                             0  .28 1.48                                                                             -85                                  Blank   H.sub.2 O                                                                            20    2 10.09                                                                              .73                                                                              0  .08 .61                                                                              -20                                  Blank   H.sub.2 O                                                                            20    8 7.95 .77                                                                              0  .04 .77                                                                               0                                   Blank   H.sub.2 O                                                                            20   14 10.55                                                                              .71                                                                              0  .23 .58                                                                              -22                                  Blank   H.sub.2 O                                                                            20   20 8.72 .21                                                                              0  .26 .70                                                                              70                                   Blank   H.sub.2 O                                                                            21    2 6.95 .20                                                                              0  .05 .88                                                                              77                                   Blank   H.sub.2 O                                                                            21    3 5.82 .49                                                                              0  .06 1.05                                                                             53                                   Blank   H.sub.2 O                                                                            21    7 8.64 .52                                                                              0  .04 .71                                                                              27                                   Blank   H.sub.2 O                                                                            21   13 7.33 .77                                                                              0  .11 .83                                                                               8                                   Blank   H.sub.2 O                                                                            21   20 8.48 .44                                                                              0  .12 .72                                                                              39                                   Blank   H.sub.2 O                                                                            22    8 7.39 .74                                                                              0  .23 .83                                                                              11                                   Blank   H.sub.2 O                                                                            22   14 7.64 .74                                                                              0  .31 .80                                                                               8                                   Blank   H.sub.2 O                                                                            22   20 8.72 .37                                                                              0  .48 .70                                                                              47                                   (NH.sub.4)2B10016                                                                     14.5%/EG                                                                             17    5 7.70 .78                                                                              71 .05 .79                                                                               2                                   (NH.sub.4)2B10016                                                                     15%/EG 18    8 7.40 .98                                                                              45 .09 .83                                                                              -18                                  (NH.sub.4)2B10016                                                                     15%/EG 18   13 7.59 .24                                                                              44 .05 .81                                                                              70                                   (NH.sub.4)2B10016                                                                     15%/EG 18   21 8.48 .17                                                                              44 .06 .72                                                                              76                                   (NH.sub.4)2B10016                                                                     10%/H.sub.2 O                                                                        21   18 9.59 .31                                                                              27 .06 .64                                                                              51                                   (NH.sub.4)2B10016                                                                     10%/H.sub.2 O                                                                        22   13 8.48 .28                                                                              27 .11 .72                                                                               61a                                 (NH.sub.4)2B407                                                                       15%/EG 18    9 8.24 .63                                                                              38 .05 .74                                                                              15                                   (NH.sub.4)2B407                                                                       15%/EG 18   24 9.42 .15                                                                              37 .04 .65                                                                              77                                   (NH.sub.4)2B407                                                                       15%/EG 19   14 9.65 .41                                                                              36 .10 .63                                                                              35                                   (NH.sub.4)2B407                                                                       10%/EG 19   22 8.83 .18                                                                              24 .12 .69                                                                              74                                   (NH.sub.4)2B407                                                                       10%/EG 20    4 10.25                                                                              .46                                                                              22 1.33                                                                              .60                                                                              23                                   (NH.sub.4)2B407                                                                       10%/EG 20    6 9.62 .29                                                                              24 .22 .64                                                                              54                                   (NH.sub.4)2B407                                                                       10%/EG 21   19 8.38 .52                                                                              25 .22 .73                                                                              29                                   (NH.sub.4)2B407                                                                       10%/H.sub.2 O                                                                        20    5 8.36 .39                                                                              24 .18 .73                                                                              47                                   (NH.sub.4)2B407                                                                       10%/H.sub.2 O                                                                        20    7 8.04 .39                                                                              23 .07 .76                                                                              49                                   (NH.sub.4)2B407                                                                       10%/H.sub.2 O                                                                        21    4 9.56 .82                                                                              22 .19 .64                                                                              -28                                  (NH.sub.4)2B407                                                                       10%/H.sub.2 O                                                                        21   21 8.58 .29                                                                              22 .06 .71                                                                              59                                   (NH.sub.4)2B407                                                                       10% in H.sub.2 O/                                                                    20    9 7.54 .40                                                                              22 .06 .81                                                                              51                                           EG (3)                                                                (NH.sub.4)2B407                                                                       10% in H.sub.2 O/                                                                    22   15 8.15 .76                                                                              23 .46 .75                                                                              -1                                           EG (3)                                                                __________________________________________________________________________     1. Predicted coke = 6.12/condensate rate (ml/min)                             2. (1coke/predicted coke) × 100%                                        EG Ethylene Glycol                                                            a. Partially plugged coke inhibitor feed line                                 (3) Ratio of H.sub.2 O/EG is 3:1                                         

A summary of the tests conducted, and results obtained are set forth inTable 2 below. Two different but well known statistical procedures areutilized in analyzing the data. A-B represents the Ansari-Bradleystatistical precedure and M-W represents the Mann-Whitney procedure,each of which utilizes its particular manner of developing itsparticular expression of confidence level.

                                      TABLE 2                                     __________________________________________________________________________    Summary of HTFA Results on Boron Antifoulants                                         # of                                                                             Coke Protection %                                                                             Statistical Analysis                               Additive                                                                              Runs                                                                             Range Avg.                                                                             SD Median                                                                            A-B (SL)*                                                                           M-W (#/CV)**                                 __________________________________________________________________________    Blank/H.sub.2 O                                                                       29 -129/79                                                                             5.2                                                                              56 11  --    --                                           (NH.sub.4)2B10016                                                                      6 -18/76                                                                              40 39 56  .239  120.5/126                                    (NH.sub.4)2B407                                                                       13 -28/77                                                                              37 30 47  .047    254/250                                    __________________________________________________________________________     *Significance level (0.05 is 95% confidence level additive protection is      greater than blank protection).                                               **Calculated number vs. critical value for 95% confidence additive            protection greater than blank protection.                                

From the data summarized in Table 2, it can be seen that both ammoniumborates tested provided averages of 32-35% reduction in coke formationvs. control tests. In addition, ammonium biborate provided protectionsignificantly greater than the control experiments at 95+% confidencelevel. The significance confidence limit for the ammonium pentaborateprotection levels was below 95% due in part to fewer experimental runsthan with ammonium biborate.

While this invention has been described with respect to particularembodiments thereof, it is apparent that numerous other forms andmodifications of this invention will be obvious to those skilled in theart. The appended claims and this invention generally should beconstrued to cover all such obvious forms and modifications which arewithin the true spirit and scope of the present invention.

We claim:
 1. A method of inhibiting the formation and deposition ofpyrolytic coke on the heated metal surfaces of the structural andassociated parts of a pyrolysis furnace which is being used to crack apetroleum feed stock to produce lower hydrocarbon fractions and saidmetal surfaces thereof having a temperature of about 1600° F. or above,which method comprises adding to the feedstock before and/or duringcracking thereof a coke inhibiting amount of an ammonium boratecompound.
 2. A method according to claim 1 wherein the hydrocarbon ismixed with steam for enhancement of the cracking thereof.
 3. A methodaccording to claim 1 wherein the ammonium borate compound is containedin a water, a glycollic, or water-glycollic carrier.
 4. A methodaccording to claim 2 wherein the ammonium borate compound is containedin a water, a glycollic, or water-glycollic carrier.
 5. A methodaccording to claim 4 wherein the ammonium borate compound is ammoniumbiborate or ammonium pentaborate.
 6. A method according to claim 1wherein the ammonium borate is added to the feedstock in an amount so asto provide from about 0.1 to 5000 parts of boron per million parts offeedstock.
 7. A method according to claim 6 wherein the hydrocarbon ismixed with steam for enhancement of the cracking thereof.
 8. A methodaccording to claim 7 wherein the ammonium borate compound is containedin a water, a glycollic, or water-glycollic carrier.
 9. A methodaccording to claim 6 wherein the ammonium borate compound is containedin a water, a glycollic, or water-glycollic carrier.
 10. A methodaccording to claim 6 wherein the ammonium borate is ammonium biborate orammonium pentaborate.
 11. A method according to claim 10 wherein thehydrocarbon is mixed with steam for enhancement of the cracking thereof.12. A method according to claim 11 wherein the ammonium borate compoundis contained in a water, a glycollic, or water-glycollic carrier.
 13. Amethod according to claim 12 wherein the ammonium borate is added to thefeedstock in an amount so as to provide from about 0.1 to 5000 parts ofboron per million parts of feedstock.
 14. A method according to claim 13wherein the glycollic carrier is ethylene glycol and/or propyleneglycol.
 15. A method according to claim 1 wherein the feedstock isethane, propane, butanes, light naphtha, heavy naphtha, gas oil ormixtures of same.
 16. A method according to claim 10 wherein theammonium borate is added to the feedstock in an amount so as to providefrom about 0.1 to 5000 parts of boron per million parts of feedstock.17. A method according to claim 16 wherein the ammonium borate compoundis selected from ammonium biborate and ammonium pentaborate.
 18. Amethod according to claim 17 wherein the hydrocarbon is mixed with steamto enhance cracking thereof.
 19. A method according to claim 18 whereinthe borate is contained in a water, glycollic or water-glycolliccarrier.
 20. In a method of inhibiting the formation and deposition ofpyrolytic coke on the heated metal surfaces of the structural andassociated parts of a pyrolysis furnace, which furnace is being used tocrack a petroleum feedstock to produce olefins, and said metal surfacesthereof having temperatures of about 1400° F. or above, which methodcomprises adding to the feedstock before and/or during cracking thereofa coke inhibiting amount of an ammonium borate compound.
 21. A methodaccording to claim 20 wherein the feedstock is ethane, propane orbutanes or mixtures thereof.
 22. A method according to claim 21 whereinthe olefins produced are ethylene, propylene, butadiene and variousmixtures thereof.
 23. A method according to claim 22 wherein thehydrocarbon is mixed with steam for enhancement of the cracking thereof.24. A method according to claim 22 wherein the ammonium borate is addedto the feedstock in an amount so as to provide from about 0.1 to 5000parts of boron per million parts of feedstock.
 25. A method according toclaim 24 wherein the ammonium borate is contained in a water, glycollicor water-glycollic carrier.
 26. A method according to claim 25 whereinthe ammonium borate is ammonium biborate.
 27. A method according toclaim 25 wherein the ammonium borate is ammonium pentaborate.
 28. Amethod according to claims 26 or 27 wherein the carrier is ethyleneglycol.